<?xml version="1.0" encoding="UTF-8"?>
<rss xmlns:dc="http://purl.org/dc/elements/1.1/" version="2.0">
<channel>
<title>Life Science Engineering (LSE)</title>
<link>https://publikationsserver.thm.de/xmlui/handle/123456789/8</link>
<description/>
<pubDate>Tue, 07 Apr 2026 10:33:11 GMT</pubDate>
<dc:date>2026-04-07T10:33:11Z</dc:date>
<item>
<title>Entwicklung und Einführung eines neuartigen dosimetrischen Formalismus in der Brachytherapie</title>
<link>https://publikationsserver.thm.de/xmlui/handle/123456789/478</link>
<description>Entwicklung und Einführung eines neuartigen dosimetrischen Formalismus in der Brachytherapie
Failing, Thomas
Bei der Brachytherapie handelt es sich um ein Spezialgebiet der Strahlentherapie, in welcher radioaktive Strahler ihre Dosis auf kurzen Distanzen direkt im bestrahlten Zielvolumen applizieren. Dieses Verfahren hat den großen Vorteil der verringerten Strahlenbelastung in der Peripherie des Zielvolumens. Aufgrund dieser speziellen geometrischen Konstellation und des Einsatzes geeigneter Strahlung bedarf die Bestimmung der absorbierten Dosis eines eigenen Formalismus, welcher sich von den sonstigen Messbedingungen der perkutanen Strahlentherapie mit Linearbeschleunigern abhebt. &#13;
Die experimentelle Kommissionierung eines Brachytherapiestrahlers oder die Verifikation einer klinischen Dosisleistungsverteilung erfordern die Messung der vom Strahler verursachten Dosisleistung in einem vorgegebenen Punkt. Zur Bestimmung der absorbierten Punktdosis mit einem realistischen Detektor müssen auf sein Signal einige Korrektionen angewandt werden. Zum einen für die unterschiedliche Energieabsorption vom Detektormaterial und Wasser sowie zum anderen zur Korrektion von Störungen des Strahlungsfeldes durch den Detektor. Dieses Verfahren wird in der Dosimetrie Sondenmethode bezeichnet. &#13;
Aufgrund der fortgeschrittenen Entwicklung in der Computertechnik können die zugehörigen Korrektionsfaktoren mithilfe von Monte-Carlo Methoden mit hinreichender Genauigkeit berechnet werden. &#13;
Die Monte-Carlo Simulation ermöglicht neben der absorbierten Dosis auch weitere dosimetrische Größen wie etwa die beschränkte Cema zu berechnen, welche unter anderem durch ihre energiedifferentielle Darstellung zum tieferen Verständnis des Ansprechvermögens von Detektoren und darauf aufbauender Optimierung beitragen können.&#13;
Ziel dieser Arbeit ist die Entwicklung und Anwendung eines Monte-Carlo basierten dosimetrischen Formalismus in der Brachytherapie auf Grundlage der beschränkten Cema. &#13;
Für klinische Anwendungen wird hiermit eine systematische quantitative Bestimmung von Korrektionsfaktoren für verschiedene Detektortypen im Zusammenspiel mit ausgewählten Brachytherapiestrahlern sowie möglichen Referenzbedingungen vorgestellt.
</description>
<pubDate>Thu, 01 Jan 2026 00:00:00 GMT</pubDate>
<guid isPermaLink="false">https://publikationsserver.thm.de/xmlui/handle/123456789/478</guid>
<dc:date>2026-01-01T00:00:00Z</dc:date>
</item>
<item>
<title>Downstream processing and analytics of adeno-associated viral vectors</title>
<link>https://publikationsserver.thm.de/xmlui/handle/123456789/472</link>
<description>Downstream processing and analytics of adeno-associated viral vectors
Meierrieks, Frederik
Viruses are crucial in biopharmaceutical applications, including their use as vaccines, oncolytic agents for cancer therapy, and gene therapy vectors to deliver therapeutic genes into cells. Among the viruses used in gene therapy, adeno‑associated viruses (AAV) are particularly promising and frequently used vectors. The growing demand for AAV, especially due to the high doses required in certain applications (≥10^14 viral genomes / kg body weight), requires advances in AAV production and purification. Efficient and simplified methods for both the production of AAV in cell culture and their purification, referred to as downstream processing (DSP), and for the corresponding analytics are essential. Furthermore, the diversity of AAV serotypes, which differ in their capsid protein composition, underscores the need for serotype‑independent purification strategies.&#13;
This thesis focuses on the development of an alternative, efficient, and serotype‑independent AAV DSP, complemented by the development of advanced analytical methods. The work centers on three key process steps: clarification, chromatographic purification and isolation, as well as chromatographic polishing. Each step has been comprehensively investigated and solutions have been proposed to address identified limitations. In addition, advanced analytical methods for AAV titer determination were developed and evaluated. The individual chapters of this thesis describe the development of analytical methods, the optimization of individual process steps, and their combination into an integrated process.&#13;
The first part of the thesis evaluates current methods for AAV titer determination and presents advanced alternatives to increase sample throughput and accelerate process development. The second part focuses on the development of a clarification process using diatomaceous earth as a filter aid. This approach improved filtration speed, simplified handling, and increased filter capacity. &#13;
The third section focuses on the separation of genome‑containing AAV (full) and genome‑deficient AAV (empty) particles by anion exchange chromatography, while the purification and isolation step is addressed in the fourth section. At that time, immunoaffinity chromatography was the only available purification and isolation method. Consequently, the development and optimization of the novel separation method described in this section relied on AAV material that was pre‑purified by immunoaffinity chromatography. In this novel approach, empty particles remain in the flow‑through during sample application and do not bind to the stationary phase. This approach reduces the required column volume and eliminates the need for precise resolution of elution peaks since empty particles are already removed during sample application.&#13;
The final chapter presents the development of a steric exclusion chromatography (SXC) method for the purification and isolation of AAV, as well as the combination of the investigated process steps into an integrated DSP. SXC proved to be a serotype‑independent and effective alternative to conventional immunoaffinity chromatography, while also eliminating intermediate steps such as concentration and buffer exchange. The entire DSP was reduced to only three steps and achieved a high AAV recovery along with a high removal of impurities.
Die vorliegende Dissertation wurde am Promotionszentrum für Ingenieurwissenschaften des Forschungscampus Mittelhessen unter Federführung der Technischen Hochschule Mittelhessen durchgeführt.
</description>
<pubDate>Wed, 01 Jan 2025 00:00:00 GMT</pubDate>
<guid isPermaLink="false">https://publikationsserver.thm.de/xmlui/handle/123456789/472</guid>
<dc:date>2025-01-01T00:00:00Z</dc:date>
</item>
<item>
<title>Phosphorus Re-dissolution and Recycling from Activated  Sludge in Full-Scale Wastewater Treatment Plants</title>
<link>https://publikationsserver.thm.de/xmlui/handle/123456789/458</link>
<description>Phosphorus Re-dissolution and Recycling from Activated  Sludge in Full-Scale Wastewater Treatment Plants
Anders, Annika
Wastewater treatment is essential to protect the environment and human health. While traditionally the focus has been on pollutant and nutrient removal, wastewater treatment plants (WWTPs) are now evolving into facilities for the additional recovery of resources. A key target for recovery is phosphorus (P), an essential element for agriculture and critical to ensure global food security. Given the finite and geopolitically vulnerable nature of global phosphate rock reserves as well as the regulatory pressure for a circular resource use, the development of methods for a sustainable nutrient management and P recovery is becoming increasingly important. Adapting the enhanced biological P removal (EBPR) process for a biological P recovery could be a promising alternative to cost- and resource intensive chemical methods. By utilizing the metabolic capability of polyphosphate accumulating organisms (PAOs) enriched in the microbial community of activated sludge (AS), P can be released from their intracellular polyP pool under anaerobic conditions. So far, most studies are based on laboratory enriched PAO cultures, limiting the real-world applicability in full-scale systems. This thesis aimed at exploring a targeted P re-dissolution approach for non-acclimated AS of full-scale WWTPs by leveraging the P cycling ability of PAOs. Key objectives included process optimization for a rapid P re-dissolution without sludge disintegration (cell lysis), identifying an efficient carbon source, and evaluating the recovery process at pilot-scale in a full-scale WWTP. Results showed that P is effectively released from non-acclimated AS within a short period of 1–4 h by adding acetate. Laboratory batch experiments revealed that AS from pure full-scale EBPR systems exhibits the highest P re-dissolution efficiency, with up to 56% of total sludge P being released. WWTPs combining EBPR and chemical P removal (CPR) show reduced P yields (19–24%), likely due to precipitant use limiting PAO activity and polyP availability. Systematic investigation of volatile fatty acid (VFA) supplementation revealed acetate at a 200 mg/L dose as the most efficient substrate for a high, fast and consistent P re-dissolution from mixed EBPR/CPR sludge. The molar P yield/C consumed ratio was 0.45. Other substrates, such as formate, propionate and butyrate were less effective. After full acetate consumption, ongoing P release was observed, which gave new insights into metabolic limitations within PAOs possibly due to polyP/glycogen depletion and disruption of the membrane potential. At pilot-scale, acetate-induced P re-dissolution in a mixed EBPR/CPR WWTP produced a P-rich stream suitable for fluidized bed precipitation using milk of lime. A precipitation efficiency of 99% was achieved. A P-enriched dolomite pellet with slow-release fertilizer characteristics was produced, potentially suitable for pH regulation in acidic soils and provision of the plant nutrients Mg, Ca and P. With a yield of 1.9% P, the recovery remained lower than in laboratory-scale, which was attributed to technical challenges in the extraction of the P-rich stream and biological P re-dissolution variability of the EBPR/CPR sludge. Overall results show that, particularly in pure EBPR systems, an acetate-mediated approach enables a rapid and targeted re-dissolution of P. Accordingly, the P-depleted AS can subsequently be returned to the aeration stage of the WWTP or disposed by co-incineration. Further research in pure EBPR systems and on long-term stability is recommended to enhance the recovery efficiency. Retrofitting WWTPs for an on-site EBPR based P recovery could contribute to a more circular P use, by providing a valuable recovery product. Concomitantly it may reduce sludge disposal costs and dependance on chemical precipitant usage.
</description>
<pubDate>Sun, 01 Jun 2025 00:00:00 GMT</pubDate>
<guid isPermaLink="false">https://publikationsserver.thm.de/xmlui/handle/123456789/458</guid>
<dc:date>2025-06-01T00:00:00Z</dc:date>
</item>
<item>
<title>Industrial-scale carbonation of alkaline residues for the final storage of CO2</title>
<link>https://publikationsserver.thm.de/xmlui/handle/123456789/441</link>
<description>Industrial-scale carbonation of alkaline residues for the final storage of CO2
Seibert, Kevin
Limiting climate change requires a substantial reduction in global greenhouse gas emissions. Mineral carbonation of alkaline residues can contribute to this by capturing CO2 and permanently binding it as carbonates. This experimental work investigated the mineral carbonation of various alkaline residues focusing on the industrial-scale implementation of this waste treatment and CO2 sequestration process using rotating drum reactors. &#13;
The research was guided by the following questions:&#13;
1)	How can the CO2 sequestration capacity of alkaline material be determined?&#13;
2)	Which effect has water on the CO2 uptake in terms of capacity and kinetics?&#13;
3)	How can the optimum amount of water be added to a rotating drum reactor?&#13;
4)	How can a rotating drum reactor be upscaled and operated to achieve the target conversion of an alkaline material?&#13;
The evalauted analytical methods to determine CO2 sequestration capacity could not accurately predict the experimentally achievable CO2 uptake. The water content of alkaline materials in fixed-bed experiments showed a considerable effect on the CO2 uptake, while in a rotating drum setup the achieved uptake was less sensitive to the water content. Water was successfully added to the rotating drum carbonation reactor while reducing the water consumption. A rotating drum reactor with a continuous feed has been upscaled to process hundreds of kilograms per hour while maintaining consistent product quality through residence time control.&#13;
While further work is needed to understand some fundamental mechanisms of mineral carbonation of alkaline residues, this research demonstrated that the process can be performed on an industrial scale.
</description>
<pubDate>Sat, 01 Mar 2025 00:00:00 GMT</pubDate>
<guid isPermaLink="false">https://publikationsserver.thm.de/xmlui/handle/123456789/441</guid>
<dc:date>2025-03-01T00:00:00Z</dc:date>
</item>
</channel>
</rss>
